JPH10139989A - Poly(lactic acid)/polysaccharide composition - Google Patents

Poly(lactic acid)/polysaccharide composition

Info

Publication number
JPH10139989A
JPH10139989A JP31570696A JP31570696A JPH10139989A JP H10139989 A JPH10139989 A JP H10139989A JP 31570696 A JP31570696 A JP 31570696A JP 31570696 A JP31570696 A JP 31570696A JP H10139989 A JPH10139989 A JP H10139989A
Authority
JP
Japan
Prior art keywords
polysaccharide
lactide
polymerization
ring
poly
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP31570696A
Other languages
Japanese (ja)
Inventor
Kenichi Nakamura
謙一 中村
Seiji Aotani
征二 青谷
Masaji Watanabe
政次 渡辺
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EKOMATETSUKU KENKYUSHO KK
SANGYO GIJUTSU KENKYUSHO KK
Original Assignee
EKOMATETSUKU KENKYUSHO KK
SANGYO GIJUTSU KENKYUSHO KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by EKOMATETSUKU KENKYUSHO KK, SANGYO GIJUTSU KENKYUSHO KK filed Critical EKOMATETSUKU KENKYUSHO KK
Priority to JP31570696A priority Critical patent/JPH10139989A/en
Publication of JPH10139989A publication Critical patent/JPH10139989A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a molding material, which is excellent in biodegradability and thermal resistance, at a low cost, by adding a polysaccharide at a specific stage of a process for carrying out ring-opening polymerization of a lactide utilizing a continuous reaction system. SOLUTION: In the process of ring-opening polymerization of a lactide, a polysaccharide powder is added at a stage where the conversion of a lactide to a polymer is 50 to 95%, and hereafter, the polymerization is continued to produce a poly(lactic acid)/polysaccharide composition. Usable polysaccharides include a cellulose substance derived from used paper, a piece of lumber from thinning, root, flue and the like; a hemicellulose derived from the husk of corn, the skin of barley, chaff and the like; starch; chitin and chitosan. A particle in an usable polysaccharide powder usually has a length along the longitudinal direction of 0.01 to 1mm. When the length is less than 0.01mm, the viscosity of the poly(lactic acid) reaction system mixed with a polysaccharide becomes too large to allow the polysaccharide to disperse with uniformity into the system, and further, such a large viscosity will result in an overload on the reaction equipment. When the length along the longitudinal direction of a polysaccharide particle is more than 1mm, a polysaccharide is difficult to be dispersed into the reaction system.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明はポリ乳酸と多糖類また
は、多糖類を主成分とする物質(以下、単に多糖類と称
する)よりなる組成物に関し、ポリ乳酸単独、あるいは
ポリ乳酸と多糖類の単純混合物に比べ生分解性、耐熱性
のより優れた成形材料を提供するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a composition comprising polylactic acid and a polysaccharide or a substance containing a polysaccharide as a main component (hereinafter, simply referred to as a polysaccharide). The present invention provides a molding material having more excellent biodegradability and heat resistance than a simple mixture of the above.

【0002】[0002]

【従来の技術】ポリ乳酸はラクチドの開環重合や、乳酸
の直接重縮合によって製造され、各種の方法で成形加工
ガ可能であり、比較的生分解性に優れていることから、
今後の環境問題に対応できるポリマーとして期待されて
いる。このポリ乳酸のコスト低減、および生分解性を一
層向上させることを目的に安価な充填剤を配合する検討
が行われて来た。 ポリ乳酸はセルロース、ヘミセルロース、澱粉、キチン
等、多糖類または、多糖類を主成分とする物質と親和性
があり、これを配合出来れば故紙の再利用や間伐材、蟹
殻、麦皮等、産業廃棄物の有効利用に繋がり、コスト低
減、生分解性の向上ガ期待される。
2. Description of the Related Art Polylactic acid is produced by ring-opening polymerization of lactide or direct polycondensation of lactic acid, and can be molded and processed by various methods, and is relatively excellent in biodegradability.
It is expected as a polymer that can respond to future environmental problems. For the purpose of reducing the cost of the polylactic acid and further improving the biodegradability, studies have been made to incorporate an inexpensive filler. Polylactic acid has an affinity for polysaccharides or substances containing polysaccharides as a main component, such as cellulose, hemicellulose, starch, and chitin. It is expected to lead to effective use of industrial waste, reduce costs and improve biodegradability.

【0003】しかし、従来ポリ乳酸と多糖類粉末を単純
に混練りする方法では多糖類を10重量%程度しか配合
できず、これを超えると多糖類の分散不良や混練り時の
ポリマーの熱分解が起こり、良好な成形体を得ることは
出来なかった。
However, in the conventional method of simply kneading polylactic acid and polysaccharide powder, only about 10% by weight of the polysaccharide can be blended. If it exceeds this, poor dispersion of the polysaccharide and thermal decomposition of the polymer during kneading will occur. And a good molded product could not be obtained.

【0004】[0004]

【本発明が解決しようとする課題】本発明は、ポリ乳酸
に多量の多糖類粉末を配合する方法を見出し、もって低
コストで、生分解性、耐熱性に優れた成形材料を提供し
ようとするものである。
The object of the present invention is to find a method of blending a large amount of polysaccharide powder with polylactic acid, and to provide a molding material which is low in cost, excellent in biodegradability and heat resistance. Things.

【0005】[0005]

【課題を解決するための手段】本発明者らは、連続反応
装置を用いてラクチドを開環重合する工程において、あ
る転化率以上に開環重合が進行した時点で多糖類粉末を
添加すると、多糖類粉末を大量に添加配合できるばかり
でなく、この配合物から得られた成型物の生分解性、耐
熱性が、単純混練り配合物から得られた成型物の生分解
性、耐熱性よりもはるかに優れていることを見出し本発
明に到達した。即ち、本発明は連続反応装置を用いてラ
クチドを開環重合する工程において、ラクチドの重合転
化率が50〜95%の時点で多糖類粉末を添加し、開環
重合を継続して製造することを特徴とするポリ乳酸と多
糖類の組成物に関するものである。
Means for Solving the Problems In the step of ring-opening polymerization of lactide using a continuous reaction apparatus, the present inventors add a polysaccharide powder when ring-opening polymerization has progressed beyond a certain conversion rate. Not only can a large amount of polysaccharide powder be added and compounded, but also the biodegradability and heat resistance of the molded product obtained from this compound are higher than the biodegradability and heat resistance of the molded product obtained from the simple kneading compound. They also found that they were much better and arrived at the present invention. That is, in the present invention, in the step of ring-opening polymerization of lactide using a continuous reaction apparatus, polysaccharide powder is added at a point in time when the polymerization conversion of lactide is 50 to 95%, and the ring-opening polymerization is continued. And a composition of polylactic acid and polysaccharide.

【0006】ラクチドの開環重合に用いられる連続反応
装置としては反応釜を複数個並べ、反応釜を順次移動し
ながら重合転化率が上昇する装置が挙げられ、このよう
な装置はラクチドの溶液開環重合に用いられる。多糖類
粉末は通常、最終釜または、一つ前の反応釜で添加され
る。
As a continuous reactor used for ring-opening polymerization of lactide, there is a device in which a plurality of reactors are arranged and a polymerization conversion rate is increased while sequentially moving the reactors. Such a device is used for opening a lactide solution. Used for ring polymerization. The polysaccharide powder is usually added in the last pot or the previous reaction pot.

【0007】より一般的なラクチドの連続開環重合装置
はベント機構付きの二軸混練り機で、ラクチドは軸内を
押し出されながら開環重合する。二軸の回転方向は同方
向回転が好ましく、このような装置を用いる場合、溶媒
は必ずしも必要としない。多糖類粉末は通常最終ベント
の手前に設けられた投入口から投入する。多糖類粉末は
ラクチドの重合転化率が50〜95%の時点、好ましく
は60〜90%の時点で添加する。
A more general continuous ring-opening polymerization apparatus for lactide is a twin-screw kneader equipped with a vent mechanism, and lactide undergoes ring-opening polymerization while being extruded in a shaft. It is preferable that the two axes rotate in the same direction. When such an apparatus is used, a solvent is not necessarily required. The polysaccharide powder is usually introduced from an inlet provided before the final vent. The polysaccharide powder is added when the polymerization conversion of lactide is 50 to 95%, preferably 60 to 90%.

【0008】重合転化率が50%未満で添加するとラク
チドの重合反応が進まなかったり、或いは反応系の流動
性が失われることがある。また、重合転化率が95%を
超えて添加すると、粉末の分散が不十分で、均一な組成
物を得ることは困難である。
If the polymerization conversion is less than 50%, the lactide polymerization reaction may not proceed or the fluidity of the reaction system may be lost. If the polymerization conversion exceeds 95%, the powder is insufficiently dispersed and it is difficult to obtain a uniform composition.

【0009】反応装置はポリマ−の熱劣化を抑え、また
分子量等の特性を調整するために窒素ガス等の不活性ガ
スで置換しておく事が好ましい。
The reactor is preferably replaced with an inert gas such as nitrogen gas in order to suppress thermal degradation of the polymer and to adjust characteristics such as molecular weight.

【0010】本発明の方法によれば、多糖類粉末を大量
に添加配合できるばかりでなく、この配合物から得られ
た成型物の生分解性、耐熱性が、単純混練り配合物から
得られた成型物の生分解性、耐熱性よりも優れているの
であるが、この理由は明白ではない。ラクチドの一部が
多糖類にグラフト重合し、その結果、ポリ乳酸と多糖類
粉末との親和性が著しく向上したものと思われる。
According to the method of the present invention, not only can a large amount of polysaccharide powder be added and blended, but also the biodegradability and heat resistance of a molded product obtained from this blend can be obtained from a simple kneaded blend. It is superior to the biodegradability and heat resistance of the molded product, but the reason is not clear. It is considered that part of lactide was graft-polymerized to the polysaccharide, and as a result, the affinity between polylactic acid and the polysaccharide powder was significantly improved.

【0011】ラクチドの開環重合では、触媒として酸化
錫、塩化第一錫、ジオクチル酸錫等の錫系触媒を通常使
用し、反応温度は190℃程度が好ましい。200℃を
超えると多糖類粉末が一部炭素化することがある。ラク
チドの開環重合に際しては、グリコリドを共重合しても
よく、また、ポリエチレングリコ−ル等のラクチドと共
重合可能な低分子量ポリマ−を改質材として共重合させ
ることもできる。
In the ring-opening polymerization of lactide, a tin catalyst such as tin oxide, stannous chloride or tin dioctylate is usually used as a catalyst, and the reaction temperature is preferably about 190 ° C. If the temperature exceeds 200 ° C., the polysaccharide powder may be partially carbonized. In the ring-opening polymerization of lactide, glycolide may be copolymerized, or a low molecular weight polymer copolymerizable with lactide such as polyethylene glycol may be copolymerized as a modifier.

【0012】多糖類の例としては、故紙、間伐材木片、
草、葉、根、綿屑等から得られるセルロ−ス性物質、コー
ン皮、麦皮、籾殻等から得られるヘミセルロース類、澱
粉類、キチン、キトサン等が挙げられる。
Examples of polysaccharides include waste paper, thinned wood,
Examples include cellulosic substances obtained from grasses, leaves, roots, cotton lint, and the like, hemicelluloses, starches, chitin, chitosan, and the like obtained from corn skin, bark, rice hulls, and the like.

【0013】多糖類粉末は長軸方向の長さが0.01〜
1mm程度のものが通常使用されるが、入手性等を考慮
すると0.02〜0.5mmが好ましい。長軸方向の長
さが0.01mm未満では、開環重合途中のポリ乳酸に
添加した時に、反応系の粘性が大きくなり過ぎ、均一に
分散出来なくなると共に、反応装置への負荷が大きくな
り過ぎる。また、長軸方向の長さが1mm以上を超える
と、反応系へ分散することが困難である。多糖類の粉末
を複数併用してよい。
The polysaccharide powder has a length in the major axis direction of 0.01 to
Although about 1 mm is usually used, it is preferably 0.02 to 0.5 mm in consideration of availability and the like. If the length in the major axis direction is less than 0.01 mm, when added to polylactic acid during ring-opening polymerization, the viscosity of the reaction system becomes too large, it becomes impossible to disperse uniformly, and the load on the reactor becomes too large. . On the other hand, if the length in the major axis direction exceeds 1 mm or more, it is difficult to disperse it in the reaction system. A plurality of polysaccharide powders may be used in combination.

【0014】ポリ乳酸の重合は反応系に水分が存在する
と、重合反応が進まなくなるので、ラクチド、及びポリ
乳酸重合途中で加える多糖類の粉体は、事前に十分乾燥
し、水分を除去しておく必要がある。
In the polymerization of polylactic acid, if water is present in the reaction system, the polymerization reaction does not proceed. Therefore, the lactide and the polysaccharide powder added during the polymerization of polylactic acid are sufficiently dried beforehand to remove the water. Need to be kept.

【0015】重合して得られたポリ乳酸と多糖類また
は、多糖類を主成分とする物質との組成物は、重合装置
の先にさらに成形機を繋ぎ、所望の成形を連続で行って
も良いが、一旦ペレタイザ−でペレット化しておき、別
途成形加工をすることも可能である。
[0015] The composition of polylactic acid and polysaccharide or a substance containing polysaccharide as a main component obtained by polymerization can be connected to a molding machine further to the end of the polymerization apparatus to perform desired molding continuously. It is good, but it is also possible to form pellets once with a pelletizer and to separately mold them.

【0016】本発明のプロセスにより、従来の方法では
実質的に不可能であった多糖類を高い割合で含有するポ
リ乳酸組成物を容易に製造することが可能となった。
The process of the present invention has made it possible to easily produce a polylactic acid composition containing a high proportion of polysaccharides, which was practically impossible with conventional methods.

【0017】[0017]

【実施例 】以下実施例に基づき本発明をさらに説明す
るが、これらは本発明を限定するものではない。
EXAMPLES The present invention will be described in further detail with reference to the following Examples, which do not limit the present invention.

【0018】[0018]

【実施例1】予め十分に乾燥し水分含有率を100pp
m以下とした、光学純度99.5%のL−ラクチドを、
L/D比が42、スクリュ−径32mmでベント機構付
き二軸押し出し型混練機の原料供給部所定の供給速度で
供給した。同時に開環重合触媒としてジオクチクル錫を
ラクチドに対し0.3%添加し、バ−レルの温度を19
0℃に保ち開環重合を開始させた。この時、第一ベント
孔より窒素ガスを供給し、第二ベント孔より排気を行っ
た。二本の回転軸は同方向回転とし、回転速度は60r
pmとした。
Example 1 Fully dried beforehand to reduce the water content to 100 pp
m or less, L-lactide having an optical purity of 99.5%
The L / D ratio was 42 and the screw diameter was 32 mm. At the same time, diocticle tin was added as a ring-opening polymerization catalyst in an amount of 0.3% to lactide, and the temperature of the barrel was reduced to 19%.
The temperature was kept at 0 ° C. to initiate ring-opening polymerization. At this time, nitrogen gas was supplied from the first vent hole, and exhaust was performed from the second vent hole. The two rotating shafts rotate in the same direction, and the rotation speed is 60r
pm.

【0019】第一ベント孔と第二ベント孔との間に粉末
供給孔を設け、重合転化率が75%の部分から、予め十
分乾燥し水分含有率が100ppm以下で、長軸方向の
長さを0.03mmに粉砕した故紙をラクチドと等量加
えた。第二ベント孔からは、排気と同時に未反応ラクチ
ドを回収した。押し出し反応装置の出口の重合反応がほ
ぼ終了した時点では、ポリ乳酸/故紙の割合が1/1の
組成物が得られた。
A powder supply hole is provided between the first vent hole and the second vent hole, and the portion having a polymerization conversion of 75% is sufficiently dried in advance to have a water content of 100 ppm or less and a length in the long axis direction. Was crushed to 0.03 mm, and the same amount of lactide as waste paper was added. Unreacted lactide was recovered from the second vent at the same time as the evacuation. At the time when the polymerization reaction at the outlet of the extrusion reaction device was almost completed, a composition having a polylactic acid / waste paper ratio of 1/1 was obtained.

【0020】このポリ乳酸と故紙組成物を引き続きペレ
タイザ−に接続し、故紙50重量%を含有するペレット
を得た。このペレットを少量採り、クロロホルムに溶解
し、不溶成分であるセルロ−ス分を分離して重量を分析
したところ、セルロ−ス分は55重量%であった。ラク
チドの一部はセルロ−スと反応し、クロロホルムに不溶
化したものと思われる。
This polylactic acid and waste paper composition were subsequently connected to a pelletizer to obtain pellets containing 50% by weight of waste paper. A small amount of this pellet was taken, dissolved in chloroform, and the cellulose component as an insoluble component was separated and analyzed for weight. As a result, the cellulose component was 55% by weight. It is considered that a part of the lactide reacted with cellulose and was insolubilized in chloroform.

【0021】このペレットを190℃で押し出し成形し
たところ、容易に厚さ0.5mmのシ−トを得た。10
cm×10cmの押し出しシ−トを65℃でコンポスト
化したところ、生分解により、3週間後には原形を留め
なかった。
When the pellets were extruded at 190 ° C., a sheet having a thickness of 0.5 mm was easily obtained. 10
When the extruded sheet of cm × 10 cm was composted at 65 ° C., the original form was not retained after 3 weeks due to biodegradation.

【0022】次に、射出成形により、肉厚0.7mmの
コップを成形した。このコップを熱湯中に入れ5分間煮
沸したが、コップの軟化、変形は認められなかった。
Next, a cup having a thickness of 0.7 mm was formed by injection molding. This cup was placed in boiling water and boiled for 5 minutes, but no softening or deformation of the cup was observed.

【0023】[0023]

【比較例1】故紙を含有しないポリ乳酸ペレットから同
様に厚さ0.5mmのシ−トと、肉厚0.7mmのコップ
を得た。
Comparative Example 1 A sheet having a thickness of 0.5 mm and a cup having a thickness of 0.7 mm were similarly obtained from polylactic acid pellets containing no waste paper.

【0024】このコップを熱湯中に入れ5分間煮沸する
と、コップは軟化、変形し、実用に供することはできな
かった。また、押し出しシ−トを65℃でコンポスト化
したところ、生分解が進み原形をとどめなくなるのに6
週間を要した。
When this cup was placed in boiling water and boiled for 5 minutes, the cup softened and deformed, and could not be put to practical use. Further, when the extruded sheet is composted at 65 ° C., biodegradation proceeds and the original form cannot be maintained.
It took a week.

【0025】[0025]

【発明の効果】特定の製造法による多糖類または、多糖
類を主成分とする物質の粉末を多量に含有するポリ乳酸
組成物は、耐熱性、生分解性に優れ、かつ低コストの成
形材料である。環境にやさしい素材を世に普及させるこ
とが可能となった。
According to the present invention, a polylactic acid composition containing a large amount of a polysaccharide or a powder of a substance containing a polysaccharide as a main component by a specific production method is excellent in heat resistance, biodegradability and low cost molding material. It is. It has become possible to spread eco-friendly materials to the world.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI // C08G 63/78 C08G 63/78 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI // C08G 63/78 C08G 63/78

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 連続反応装置を用いてラクチドを開環重
合する工程において、ラクチドの重合転化率が50〜9
5%の時点で多糖類または、多糖類をを主成分とする粉
末を添加し、開環重合を継続して製造することを特徴と
する、ポリ乳酸と多糖類または、多糖類を主成分とする
物質との組成物。
In the step of subjecting lactide to ring-opening polymerization using a continuous reactor, the polymerization conversion of lactide is 50 to 9%.
At the time of 5%, a polysaccharide or a powder containing a polysaccharide as a main component is added, and the ring-opening polymerization is continued to produce. Composition with a substance.
JP31570696A 1996-11-13 1996-11-13 Poly(lactic acid)/polysaccharide composition Pending JPH10139989A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31570696A JPH10139989A (en) 1996-11-13 1996-11-13 Poly(lactic acid)/polysaccharide composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31570696A JPH10139989A (en) 1996-11-13 1996-11-13 Poly(lactic acid)/polysaccharide composition

Publications (1)

Publication Number Publication Date
JPH10139989A true JPH10139989A (en) 1998-05-26

Family

ID=18068569

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31570696A Pending JPH10139989A (en) 1996-11-13 1996-11-13 Poly(lactic acid)/polysaccharide composition

Country Status (1)

Country Link
JP (1) JPH10139989A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002348366A (en) * 2001-03-19 2002-12-04 Toyobo Co Ltd Manufacturing method of biodegradable polyester
CN100431623C (en) * 2006-10-23 2008-11-12 天津大学 Method for preparing 3D porous bracket of chitosan - copolymer of poly lactic acid
KR101417413B1 (en) * 2012-11-16 2014-07-08 현대자동차주식회사 A method for manufacturing natural fiber poly lactic acid composite materials
CN111019099A (en) * 2019-12-02 2020-04-17 华南理工大学 Chitosan grafted polylactic acid copolymer and preparation method and application thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002348366A (en) * 2001-03-19 2002-12-04 Toyobo Co Ltd Manufacturing method of biodegradable polyester
CN100431623C (en) * 2006-10-23 2008-11-12 天津大学 Method for preparing 3D porous bracket of chitosan - copolymer of poly lactic acid
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CN111019099A (en) * 2019-12-02 2020-04-17 华南理工大学 Chitosan grafted polylactic acid copolymer and preparation method and application thereof
CN111019099B (en) * 2019-12-02 2021-12-21 华南理工大学 Chitosan grafted polylactic acid copolymer and preparation method and application thereof

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